Study of flow fluctuation in the thermal bubble pump tube

Q3 Engineering
Ali Benhmidène, Rabeb Jemaii, K. Hidouri, B. Chaouachi
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引用次数: 0

Abstract

In the present work, we were interested in the study of the oscillatory phenomenon of ammonia-water two-phase flow inside the bubble pump of absorption-diffusion refrigerators. In fact, flow instability can reduce the efficiency of the bubble pump. The simulation of two-phase flow in the bubble pump is conducted by using the drift flow model. Balance equations of the drift flow model and their closure relationships, as well as the numerical method, were developed. The numerical resolution allowed defining the void fraction, the liquid and vapor velocities, the pressure, and the mixing enthalpy against time. The effect of heat flux received by the bubble pump is simulated in the transitional regime. Simulated results of the vapor, liquid, and mass velocities show a flow fluctuation at the beginning of the operation. The duration of the fluctuation increase from 6 s to 12 s by reducing the heat flux from 5 to 2 kW/m².The void fraction profile makes it possible to distinguish that the slug and churn regimes are those which dominate the pump’s operating regime for a heat flux of 2 and 3 kW/m². The pumping action is influenced by the heat flux. A maximum of 10 kW/m² value of heat flux is defined for an obtained minimum of the pumping action.
热泡泵管内流量波动的研究
本文对吸收-扩散制冷机气泡泵内氨-水两相流动的振荡现象进行了研究。实际上,流动不稳定会降低气泡泵的效率。采用漂移流模型对气泡泵内两相流动进行了模拟。建立了漂移流模型的平衡方程及其闭合关系,并给出了数值计算方法。数值分辨率允许定义空隙率、液体和蒸汽速度、压力和随时间的混合焓。在过渡状态下,模拟了气泡泵接收的热流密度的影响。蒸汽、液体和质量速度的模拟结果表明,在操作开始时存在流量波动。热流密度从5 kW/m²降低到2 kW/m²,波动持续时间从6 s增加到12 s。在热流密度为2和3kw /m²的情况下,通过空隙率曲线可以区分段塞流和搅拌流是影响泵运行的主要因素。泵送作用受热流的影响。对于获得的最小泵送作用,定义了最大10 kW/m²的热流密度值。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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